CN101152992A - Emulsifying blasting agent produced on blasting agent mixing vehicle - Google Patents
Emulsifying blasting agent produced on blasting agent mixing vehicle Download PDFInfo
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- CN101152992A CN101152992A CNA2006100479539A CN200610047953A CN101152992A CN 101152992 A CN101152992 A CN 101152992A CN A2006100479539 A CNA2006100479539 A CN A2006100479539A CN 200610047953 A CN200610047953 A CN 200610047953A CN 101152992 A CN101152992 A CN 101152992A
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Abstract
The present invention provides an emulsified explosive produced on an explosive mixture vehicle. The components contain: 63 to 85 weight percent of inorganic oxidizer salt, 10 to 25 weight percent of water, 3 to 10 weight percent of hydrocarbon fuel, 0.5 to 2.5 weight percent of emulsifier, and 0.01 to 0.15 weight percent of sensitizer. The components of the emulsifier has the above formula; wherein, n is equal to 5 to 30; R1 is the alkyl of C2-C12; R2 is the alkyl of C5-C80; R3 is the alkyl of C8- C20. The contents of components of the emulsifier are: 30 to 70 weight percent of (I), 10 to 50 weight percent of (II), 10 to 40 weight percent of (III), and 10 to 20 weight percent of (IV). The composite macro-molecule emulsifier is used on an explosive mixture vehicle, thus lowering the cost of emulsifier; the use of complex technology solves the defects of excessively high viscosity and inefficient hydrophilicity of single macro-molecule emulsifier, improves emulsion effects and improves the stability of latex matrix; the technology greatly improves the storage life and water resistance of emulsified explosives; the emulsified explosive has no detonator sensitivity, but has safety and reliability of production, and good detonation performances.
Description
Technical field
The present invention relates to a kind of emulsion explosive, the emulsion explosive of especially on blasting agent mixing vehicle, producing.
Background technology
The emulsion explosive of preparation processing is the scene of ore deposit explosion in the open on the blasting agent mixing vehicle, carries out the emulsion explosive of continuous emulsification and sensitization preparation on blasting agent mixing vehicle, is delivered directly to simultaneously in the big gun hole.The emulsion explosive of blasting agent mixing vehicle preparation is water-in-oil (W/O) type insensitiveness emulsion explosive, no cap-sensitivity, it consists of inorganic salt solution, hydrocarbon fuel, emulsifying agent and the sensitizing agent component that oxygen can be provided, and it is good to have a security, preparation technology is simple, characteristics such as detonation property excellence.
The emulsion explosive of producing on the blasting agent mixing vehicle belongs to non-thermodynamic stable system, the supersaturated solution that is dispersed in oil phase exists with the small supercooled liquid form of dripping, very easily assemble the crystallization breakdown of emulsion, be to need the basic problem that solves in this research field so improve Emulsion Explosive Stability always.20 days Sp-80 emulsifying agent shelf liveves are adopted in the vehicle made emulsification blasting optimization of formulation research that " engineering explosion "-1998.4 (2) 30-32 openly report.The feasibility study of the application BCRH-15 type emulsification blasting agent mixing vehicle that " China molybdenum industry "-1995.19 (6) 33-38 openly report proposed water resisting property more than 48 hours.The development of DRHC that Changsha Mine Inst's quarterly-1991.11 (3) 18-25 openly report series emulsion explosive with use, be generally for 2～8 weeks the storage period of described explosive, the highest can be greater than half a year.USP 572096 patent disclosures be the emulsion explosive of emulsifying agent preparation with the sorbitol ester class, the shelf lives is 85 days.Single low molecule emulsifying agent or macromolecule emulsifier are all adopted in these researchs, the emulsifying film intensity that forms is lower, so Stability of Emulsion Explosives still can not get the demand for development that satisfied effect, particularly shelf lives, water resisting property and security can not be satisfied blasting works.
Summary of the invention
The objective of the invention is to overcome above shortcoming, improve shelf lives, water resisting property and security with the emulsion explosive of blasting agent mixing vehicle preparation.
The consisting of of the emulsion explosive of producing on the blasting agent mixing vehicle of the present invention (by weight percentage):
Inorganic oxidant salt 63%～85%,
Water 10%～25%,
Hydrocarbon fuel 3%～10%,
Emulsifying agent 0.5%～2.5%,
Sensitizing agent 0.01%～0.15%;
The component of described emulsifying agent is:
(IV) water
N=5 in the formula～30, R
1Be C
2～C
12Alkyl, R
2Be C
5～C
80Alkyl, R
3Be C
8～C
20Alkyl;
Each components contents of emulsifying agent (by weight percentage) is: (I): 30%～70%, (II): 10%～50%, (III): 10%～40%, (IV) 10%～20%.
Inorganic oxidant salt of the present invention is the mixture that ammonium nitrate and SODIUMNITRATE are formed, and its weight percent: ammonium nitrate is 85%～95%, and SODIUMNITRATE is 5%～15%.
Hydrocarbon fuel of the present invention is combined by machine oil and diesel oil, can be by 68
#Machine oil and one or more diesel oil are formed its content (with the weight percent meter of emulsion explosive): 68
#Machine oil is 1.5%～5%, 0
#Diesel oil is 0%～2.5% ,-10
#Diesel oil is 0%～1.5% ,-35
#Diesel oil is 0%～1.5%.
The composition of emulsion explosive of the present invention is preferably (by weight percentage): inorganic oxidant salt: 72%～78%, and water: 14%～20%, hydrocarbon fuel: 4.5%～7%, emulsifying agent: 1.3%～1.8%, sensitizing agent: 0.03%～0.12%.
The synthetic method of the used emulsifying agent of emulsion explosive of the present invention is as follows, with terminal hydroxy group Soxylat A 25-7 20%～40%, polyisobutene acid anhydrides or polyisobutene carboxylic acid 20%～40% and (concentration weight percent 30%～60%) NaOH or 0.3%～1.2% mixing of the KOH aqueous solution, heating vacuumizes, 150～300 ℃ ,-0.02～-the 0.08MPa condition under esterification after 3～8 hours, be cooled to 60～120 ℃, add (concentration weight percent 30%～70%) alkylsulphonic acid salt brine solution 20%～50%, normal pressure constant temperature is 1～3 hour again, and reaction finishes.
The present invention is applied to blasting agent mixing vehicle with Soxylat A 25-7 and polyisobutene acid anhydrides or polyisobutene carboxylic esterification product and alkylsulfonate composite high-molecular emulsifying agent first, has reduced the emulsifying agent cost; Adopt compounded technology, solved that single macromolecule emulsifier viscosity is too high, the insufficient shortcoming of wetting ability, improved emulsifying effectiveness, latex particle size mean value is reduced to below the 0.1 μ m, makes explosive have the micro emulsion voltinism; By in emulsion process, forming the netted interfacial film of composite host, increased emulsification film strength and thickness, improved emulsion matrix stability, the shelf lives and the water resisting property of emulsion explosive are increased substantially, this emulsion explosive does not have cap-sensitivity, and production safety is reliable, good detonation performances.
Embodiment
The present invention is a kind ofly loading in mixture the emulsion explosive of producing on the car, its preparation method is different from emulsifying process and continuous processing at general intermittence, be after terrestrial station prepares water and oil phase at a certain temperature, pump into respectively in the water groove and oil phase groove of blasting agent mixing vehicle, it is on-the-spot that blasting agent mixing vehicle is reached quick-fried district, carries out continuous emulsification, sensitization, pumping and directly pack in the big gun hole on blasting agent mixing vehicle.
The embodiment of emulsion explosive of the present invention (component and performance) sees Table 1.
Table 1 embodiment of the invention (with the emulsion explosive weight percent meter):
| Embodiment 1 | Embodiment 2 | Embodiment 3 | Embodiment 4 | |
| Ammonium nitrate SODIUMNITRATE water machine oil diesel oil emulsifier sensitizing agent | 68％ 9.5％ 16％ 3.25％ 2.15％ 1.0％ 0.1％ | 68％ 9.5％ 16％ 2.25％ 3.15％ 1.0％ 0.1％ | 68％ 9.5％ 16％ 3.0％ 1.9％ 1.5％ 0.1％ | 68％ 9.5％ 16％ 2.0％ 2.9％ 1.5％ 0.1％ |
| Cap-sensitivity | Do not have | Do not have | Do not have | Do not have |
| Density of Emulsion Explosive | 1.25g/cm 3 | 1.25g/cm 3 | 1.25g/cm 3 | 1.25g/cm 3 |
| Explosion velocity (m/s) | 5006 | 5105 | 5143 | 5387 |
| Water resisting property | 〉=one month | 〉=one month | 〉=one month | 〉=one month |
| The emulsion explosive shelf lives | 〉=one year | 〉=one year | 〉=one year | 〉=one year |
| The emulsion matrix shelf lives | 〉=a year and a half | 〉=a year and a half | 〉=a year and a half | 〉=a year and a half |
Emulsion explosive and the detection method of emulsion matrix shelf lives listed in the table 1 have adopted high low temperature round-robin test, be about to sample subzero 20 ℃ freezing 16 hours, place 50 ℃ of constant temperature 8 hours as once circulation then, the emulsion explosive of the present invention's preparation and emulsion matrix cycle index are respectively up to 23 times with 30 times (general high cold cycle 20 shelf lives can above 1 year).
Comparative example 1 (adopting the Sp-80 emulsifying agent):
Ammonium nitrate: 78～82wt%
Water: 16～20wt%
Sodium Nitrite: 0.1wt%
Oil: 4.2～5.0wt%
Sp-80： 1.0～1.2wt％
Shelf lives: 20 days
Comparative example 2 (" China molybdenum industry " report):
The emulsion explosive that loads in mixture the mixed system of car soaks more than 48 hours in the sour water of PH-2-3.
Comparative example 3:(Changsha Mine Inst quarterly report)
With the matching used DRHC series of emulsification blasting agent mixing vehicle emulsion explosive, described explosive
Be generally for 2～8 weeks storage period, the highest can be greater than half a year.
Comparative example 4:(USP 572096 patents)
With the sorbitol ester class is the emulsion explosive of emulsifying agent preparation, and the shelf lives is 85 days.
Claims (5)
1. the emulsion explosive of producing on the blasting agent mixing vehicle is characterized in that consist of (by weight percentage) of this emulsion explosive:
Inorganic oxidant salt 63%～85%,
Water 10%～25%,
Hydrocarbon fuel 3%～10%,
Emulsifying agent 0.5%～2.5%,
Sensitizing agent 0.01%～0.15%;
The component of described emulsifying agent is:
(III)R
3-SO
3Na
(IV) water
N=5 in the formula～30, R
1Be C
2～C
12Alkyl, R
2Be C
5～C
80Alkyl, R
3Be C
8～C
20Alkyl;
Each components contents of emulsifying agent (by weight percentage) is: (I): 30%～70%, (II):
10％～50％，(III)：10％～40％，(IV)10％～20％。
2. emulsion explosive according to claim 1 is characterized in that described inorganic oxidant salt is the mixture that ammonium nitrate and SODIUMNITRATE are formed, and its weight percent: ammonium nitrate is 85%～95%, and SODIUMNITRATE is 5%～15%.
3. emulsion explosive according to claim 1 is characterized in that described hydrocarbon fuel is combined by machine oil and diesel oil.
4. emulsion explosive according to claim 3 is characterized in that described hydrocarbon fuel is by 68
#Machine oil and one or more diesel oil are formed its content (with the weight percent meter of emulsion explosive): 68
#Machine oil is 1.5%～5%, 0
#Diesel oil is 0%～2.5% ,-10
#Diesel oil is 0%～1.5% ,-35
#Diesel oil is 0%～1.5%.
5. emulsion explosive according to claim 1, the composition that it is characterized in that this emulsion explosive is preferably (by weight percentage): inorganic oxidant salt: 72%～78%, water: 14%～20%, hydrocarbon fuel: 4.5%～7%, emulsifying agent: 1.3%～1.8%, sensitizing agent: 0.03%～0.12%.
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| CN2006100479539A CN101152992B (en) | 2006-09-29 | 2006-09-29 | Emulsifying blasting agent produced on blasting agent mixing vehicle |
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| CN2006100479539A CN101152992B (en) | 2006-09-29 | 2006-09-29 | Emulsifying blasting agent produced on blasting agent mixing vehicle |
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| CN101152992A true CN101152992A (en) | 2008-04-02 |
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Cited By (8)
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| CN102424644A (en) * | 2011-09-09 | 2012-04-25 | 福建省民爆化工股份有限公司 | High-quality expanded ammonium nitrate and preparation method thereof |
| CN102643151A (en) * | 2012-05-11 | 2012-08-22 | 薛世忠 | Emulsified base distribution station |
| CN102675010A (en) * | 2012-05-15 | 2012-09-19 | 鞍钢集团矿业公司 | Bulk waterproof emulsion explosive and preparation method thereof |
| CN102675009A (en) * | 2012-05-15 | 2012-09-19 | 鞍钢集团矿业公司 | Loose-packed waterproof latex heavy ammonium nitrate oil explosive and preparation method thereof |
| CN102731231A (en) * | 2012-07-09 | 2012-10-17 | 煤炭科学研究总院爆破技术研究所 | Sensitizer and method for preparing field mixed vehicle-made emulsion explosive by using sensitizer |
| CN102936027A (en) * | 2011-08-15 | 2013-02-20 | 倪欧琪 | Method for detonation synthesis of particle size controllable nano-cerium oxide |
| CN103011271A (en) * | 2012-11-20 | 2013-04-03 | 南京理工大学 | Method for synthesizing spherical nano-titanium-oxide by using detonation method in grain diameter controllable manner |
| CN103011279A (en) * | 2012-11-20 | 2013-04-03 | 南京理工大学 | Method for synthesizing spherical nano-zirconia by using detonation method in grain diameter controllable manner |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN1156137A (en) * | 1995-11-08 | 1997-08-06 | 帝国化学工业(加拿大)有限公司 | Emulgent for explosive composition |
| CN1067039C (en) * | 1996-01-17 | 2001-06-13 | 中国石油化工总公司 | Emulsifier for emulsified explosive and its preparation process |
| CN1164533C (en) * | 2001-01-05 | 2004-09-01 | 中国石油化工股份有限公司 | Emulsified explosive |
| CN1291952C (en) * | 2001-12-20 | 2006-12-27 | 日本化药株式会社 | Explosive |
| CN1259290C (en) * | 2003-10-24 | 2006-06-14 | 中国石油化工股份有限公司 | Emulsifier for powdered emulsified explosive and its prepn process |
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2006
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| CN102936027A (en) * | 2011-08-15 | 2013-02-20 | 倪欧琪 | Method for detonation synthesis of particle size controllable nano-cerium oxide |
| CN102936027B (en) * | 2011-08-15 | 2014-07-23 | 倪欧琪 | Method for detonation synthesis of particle size controllable nano-cerium oxide |
| CN102424644A (en) * | 2011-09-09 | 2012-04-25 | 福建省民爆化工股份有限公司 | High-quality expanded ammonium nitrate and preparation method thereof |
| CN102424644B (en) * | 2011-09-09 | 2013-11-06 | 福建省民爆化工股份有限公司 | Expanded ammonium nitrate and preparation method thereof |
| CN102643151A (en) * | 2012-05-11 | 2012-08-22 | 薛世忠 | Emulsified base distribution station |
| CN102643151B (en) * | 2012-05-11 | 2016-05-11 | 青岛拓极采矿服务有限公司 | Emulsified bases dispensing station |
| CN102675010B (en) * | 2012-05-15 | 2014-08-06 | 鞍钢集团矿业公司 | Bulk waterproof emulsion explosive and preparation method thereof |
| CN102675010A (en) * | 2012-05-15 | 2012-09-19 | 鞍钢集团矿业公司 | Bulk waterproof emulsion explosive and preparation method thereof |
| CN102675009A (en) * | 2012-05-15 | 2012-09-19 | 鞍钢集团矿业公司 | Loose-packed waterproof latex heavy ammonium nitrate oil explosive and preparation method thereof |
| CN102675009B (en) * | 2012-05-15 | 2015-04-01 | 鞍钢集团矿业公司 | Loose-packed waterproof latex heavy ammonium nitrate oil explosive and preparation method thereof |
| CN102731231A (en) * | 2012-07-09 | 2012-10-17 | 煤炭科学研究总院爆破技术研究所 | Sensitizer and method for preparing field mixed vehicle-made emulsion explosive by using sensitizer |
| CN102731231B (en) * | 2012-07-09 | 2015-06-03 | 中煤科工集团淮北爆破技术研究院有限公司 | Sensitizer and method for preparing field mixed vehicle-made emulsion explosive by using sensitizer |
| CN103011279A (en) * | 2012-11-20 | 2013-04-03 | 南京理工大学 | Method for synthesizing spherical nano-zirconia by using detonation method in grain diameter controllable manner |
| CN103011271B (en) * | 2012-11-20 | 2015-07-01 | 南京理工大学 | Method for synthesizing spherical nano-titanium-oxide by using detonation method in grain diameter controllable manner |
| CN103011279B (en) * | 2012-11-20 | 2015-07-01 | 南京理工大学 | Method for synthesizing spherical nano-zirconia by using detonation method in grain diameter controllable manner |
| CN103011271A (en) * | 2012-11-20 | 2013-04-03 | 南京理工大学 | Method for synthesizing spherical nano-titanium-oxide by using detonation method in grain diameter controllable manner |
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Address after: 114001 Liaoning Province, the eastern part of the Anshan iron green street, No. 27 Patentee after: ANGANG GROUP MINING ENGINEERING Corp. Address before: 114001 Liaoning Province, the eastern part of the Anshan iron green street, No. 27 Patentee before: INST OF MINING DESIGN ANSHAN IRON AND STEEL Group Corp. |
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